CA2694847C - Systeme et methode sans aucune decharge de liquide - Google Patents
Systeme et methode sans aucune decharge de liquide Download PDFInfo
- Publication number
- CA2694847C CA2694847C CA2694847A CA2694847A CA2694847C CA 2694847 C CA2694847 C CA 2694847C CA 2694847 A CA2694847 A CA 2694847A CA 2694847 A CA2694847 A CA 2694847A CA 2694847 C CA2694847 C CA 2694847C
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- solids
- water
- gas
- liquid
- Prior art date
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- 238000000034 method Methods 0.000 title claims abstract description 96
- 239000007788 liquid Substances 0.000 title claims abstract description 72
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 273
- 239000007787 solid Substances 0.000 claims abstract description 196
- 239000000567 combustion gas Substances 0.000 claims abstract description 71
- 239000000203 mixture Substances 0.000 claims abstract description 30
- 238000002156 mixing Methods 0.000 claims abstract description 18
- 238000002347 injection Methods 0.000 claims abstract description 16
- 239000007924 injection Substances 0.000 claims abstract description 16
- 239000012267 brine Substances 0.000 claims abstract description 15
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims abstract description 15
- 230000001483 mobilizing effect Effects 0.000 claims abstract description 3
- 239000007789 gas Substances 0.000 claims description 110
- 239000000446 fuel Substances 0.000 claims description 55
- 238000002485 combustion reaction Methods 0.000 claims description 47
- 239000002002 slurry Substances 0.000 claims description 39
- 238000004519 manufacturing process Methods 0.000 claims description 30
- 238000012546 transfer Methods 0.000 claims description 27
- 238000000605 extraction Methods 0.000 claims description 23
- 238000007599 discharging Methods 0.000 claims description 18
- 239000012071 phase Substances 0.000 claims description 18
- 239000000463 material Substances 0.000 claims description 17
- 239000002245 particle Substances 0.000 claims description 17
- 239000007800 oxidant agent Substances 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 13
- 229930195733 hydrocarbon Natural products 0.000 claims description 13
- 150000002430 hydrocarbons Chemical class 0.000 claims description 13
- 238000011084 recovery Methods 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 12
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 11
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 11
- 239000004571 lime Substances 0.000 claims description 11
- 239000010802 sludge Substances 0.000 claims description 10
- 238000001704 evaporation Methods 0.000 claims description 8
- 239000007791 liquid phase Substances 0.000 claims description 3
- 239000010865 sewage Substances 0.000 claims description 3
- 230000002708 enhancing effect Effects 0.000 claims 2
- 238000005192 partition Methods 0.000 claims 2
- 239000002699 waste material Substances 0.000 abstract description 6
- 239000010808 liquid waste Substances 0.000 abstract description 2
- 230000008569 process Effects 0.000 description 49
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 20
- 239000012530 fluid Substances 0.000 description 17
- 239000003027 oil sand Substances 0.000 description 15
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 14
- 239000010426 asphalt Substances 0.000 description 12
- 239000002562 thickening agent Substances 0.000 description 12
- 229910052799 carbon Inorganic materials 0.000 description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 10
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 10
- 229910002092 carbon dioxide Inorganic materials 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 10
- 239000003245 coal Substances 0.000 description 10
- 238000007254 oxidation reaction Methods 0.000 description 10
- 235000019738 Limestone Nutrition 0.000 description 9
- GBAOBIBJACZTNA-UHFFFAOYSA-L calcium sulfite Chemical compound [Ca+2].[O-]S([O-])=O GBAOBIBJACZTNA-UHFFFAOYSA-L 0.000 description 9
- 235000010261 calcium sulphite Nutrition 0.000 description 9
- 239000006028 limestone Substances 0.000 description 9
- 230000003647 oxidation Effects 0.000 description 9
- 239000002006 petroleum coke Substances 0.000 description 9
- 239000004215 Carbon black (E152) Substances 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 8
- 239000000428 dust Substances 0.000 description 8
- 239000010440 gypsum Substances 0.000 description 8
- 229910052602 gypsum Inorganic materials 0.000 description 8
- 230000010354 integration Effects 0.000 description 8
- 238000005065 mining Methods 0.000 description 8
- 239000003921 oil Substances 0.000 description 8
- 239000003345 natural gas Substances 0.000 description 7
- 230000008020 evaporation Effects 0.000 description 6
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 6
- 229920006395 saturated elastomer Polymers 0.000 description 6
- 239000002910 solid waste Substances 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 5
- 239000013078 crystal Substances 0.000 description 5
- 238000004821 distillation Methods 0.000 description 5
- 239000000295 fuel oil Substances 0.000 description 5
- XZPVPNZTYPUODG-UHFFFAOYSA-M sodium;chloride;dihydrate Chemical compound O.O.[Na+].[Cl-] XZPVPNZTYPUODG-UHFFFAOYSA-M 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 229910052717 sulfur Inorganic materials 0.000 description 5
- 239000011593 sulfur Substances 0.000 description 5
- 239000005995 Aluminium silicate Substances 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 235000012211 aluminium silicate Nutrition 0.000 description 4
- 238000005188 flotation Methods 0.000 description 4
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 238000007792 addition Methods 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 3
- 239000000571 coke Substances 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 239000012153 distilled water Substances 0.000 description 3
- 239000010459 dolomite Substances 0.000 description 3
- 229910000514 dolomite Inorganic materials 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000005201 scrubbing Methods 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010794 Cyclic Steam Stimulation Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 238000010796 Steam-assisted gravity drainage Methods 0.000 description 2
- 239000002956 ash Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000011552 falling film Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000036571 hydration Effects 0.000 description 2
- 238000006703 hydration reaction Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 229910052815 sulfur oxide Inorganic materials 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- -1 MFT Substances 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000009412 basement excavation Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000000378 calcium silicate Substances 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011335 coal coke Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000012938 design process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000009969 flowable effect Effects 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 239000013529 heat transfer fluid Substances 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 235000003642 hunger Nutrition 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 229910003480 inorganic solid Inorganic materials 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000009919 sequestration Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1853—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines coming in direct contact with water in bulk or in sprays
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
La présente invention est un système et une méthode de production dun mélange de vapeur et de gaz de combustion dans un générateur de vapeur rotatif à contact direct employant de leau à forte teneur en solides et ne produisant pas de décharge de déchets liquides. Linvention comprend le retrait des solides ayant une teneur en eau contrôlable dans une forme empilable qui peut supporter la circulation. Le système comprend un tambour rotatif à pression contrôlée longitudinalement installé selon une pente et ayant une section dinjection dénergie, une section de production de vapeur, une section dinjection deau et une section de décharge. La section de décharge peut comprendre un élément rotatif secondaire de mélange et mobilisation servant à décharger les solides produits. Le système peut être intégré à une installation de RAH qui comprend des évaporateurs deau qui produisent une saumure concentrée ou une installation dextraction de pétrole ouverte qui produit des résidus non séparés afin de consommer les déchets de liquide de décharge et produire de la vapeur, de la chaleur et des déchets solides stables.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2694847A CA2694847C (fr) | 2008-02-26 | 2010-02-26 | Systeme et methode sans aucune decharge de liquide |
| CA2715619A CA2715619A1 (fr) | 2009-11-12 | 2010-09-13 | Generation de vapeur par contact direct de la vapeur |
| US12/907,009 US8646415B2 (en) | 2009-03-18 | 2010-10-18 | System and method for zero liquid discharge |
Applications Claiming Priority (12)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/037,703 US7814867B2 (en) | 2008-02-26 | 2008-02-26 | Reaction chamber for a direct contact rotating steam generator |
| CA2,655,353 | 2009-02-26 | ||
| CA2655353A CA2655353C (fr) | 2008-02-26 | 2009-02-26 | Generateur de vapeur rotatif a contact direct pour la production de vapeur au moyen d'eau de qualite mediocre et sans decharge de liquide |
| CA002665751A CA2665751A1 (fr) | 2008-05-12 | 2009-05-12 | Procede integre de production de vapeur pour recuperation amelioree du petrole |
| CA2,665,751 | 2009-05-12 | ||
| CA002665747A CA2665747A1 (fr) | 2008-05-12 | 2009-05-12 | Utilisation des boues excedentaires et des eaux a fins residus d'installations petrolieres pour l'obtention d'eau chaude et de vapeur destinees a la production de bitume |
| CA2,665,747 | 2009-05-12 | ||
| CA2,684,817 | 2009-11-12 | ||
| CA2684817A CA2684817C (fr) | 2008-12-12 | 2009-11-12 | Procede de production de vapeur et installation de recuperation amelioree de petrole |
| CA2686140A CA2686140C (fr) | 2008-12-12 | 2009-11-23 | Un systeme et une methode de recuperation de l'eau des residus |
| CA2,686,140 | 2009-11-23 | ||
| CA2694847A CA2694847C (fr) | 2008-02-26 | 2010-02-26 | Systeme et methode sans aucune decharge de liquide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2694847A1 CA2694847A1 (fr) | 2010-08-26 |
| CA2694847C true CA2694847C (fr) | 2018-04-10 |
Family
ID=40997084
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2655353A Active CA2655353C (fr) | 2008-02-26 | 2009-02-26 | Generateur de vapeur rotatif a contact direct pour la production de vapeur au moyen d'eau de qualite mediocre et sans decharge de liquide |
| CA2694847A Active CA2694847C (fr) | 2008-02-26 | 2010-02-26 | Systeme et methode sans aucune decharge de liquide |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2655353A Active CA2655353C (fr) | 2008-02-26 | 2009-02-26 | Generateur de vapeur rotatif a contact direct pour la production de vapeur au moyen d'eau de qualite mediocre et sans decharge de liquide |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US7814867B2 (fr) |
| CA (2) | CA2655353C (fr) |
Families Citing this family (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8561702B2 (en) * | 2007-02-10 | 2013-10-22 | Vast Power Portfolio, Llc | Hot fluid recovery of heavy oil with steam and carbon dioxide |
| US8468980B2 (en) * | 2008-02-26 | 2013-06-25 | Ex-Tar Technologies, Inc. | Direct contact rotating steam generator using low quality water with zero liquid discharge |
| US20110056442A1 (en) * | 2008-02-26 | 2011-03-10 | Ex-Tar Technologies, Inc. | Reaction chamber for a direct contact rotating steam generator |
| KR101385101B1 (ko) * | 2008-06-27 | 2014-04-15 | 동부대우전자 주식회사 | 가스식 건조기의 밸브 제어 방법 |
| JP5316290B2 (ja) * | 2008-08-05 | 2013-10-16 | 三菱マテリアル株式会社 | トリクロロシラン製造装置及び製造方法 |
| US8646415B2 (en) * | 2009-03-18 | 2014-02-11 | Ex-Tar Technologies | System and method for zero liquid discharge |
| WO2011133785A1 (fr) * | 2010-04-23 | 2011-10-27 | Conocophillips Company | Traitement de l'eau à l'aide de générateur de vapeur d'eau directe |
| US20120012036A1 (en) * | 2010-07-15 | 2012-01-19 | Shaw John R | Once Through Steam Generator |
| US9375725B2 (en) | 2010-12-03 | 2016-06-28 | Bepex International, Llc | System and method for the treatment of oil sands |
| US9249972B2 (en) * | 2013-01-04 | 2016-02-02 | Gas Technology Institute | Steam generator and method for generating steam |
| US9200800B2 (en) * | 2014-01-17 | 2015-12-01 | General Electric Company | Method and system for steam generation and purification |
| CA2853115C (fr) | 2014-05-29 | 2016-05-24 | Quinn Solutions Inc. | Appareil, systeme et methode de controle de la production de gaz de combustion dans la generation de vapeur directe destines a la recuperation de petrole |
| CA2976575A1 (fr) | 2016-08-25 | 2018-02-25 | Conocophillips Company | Configuration de puits en vue de la coinjection |
| US11156072B2 (en) | 2016-08-25 | 2021-10-26 | Conocophillips Company | Well configuration for coinjection |
| CN111875221A (zh) * | 2020-07-08 | 2020-11-03 | 中国神华煤制油化工有限公司 | 污泥干化方法和污泥干化系统 |
| CN113485499B (zh) * | 2021-08-26 | 2022-11-01 | 润电能源科学技术有限公司 | 一种煤质工况变化的给煤调控方法 |
| CN114646019A (zh) * | 2022-03-10 | 2022-06-21 | 绥化学院 | 玉米深加工过程废水废汽中水分及热能的回收利用方法 |
| WO2024012886A1 (fr) * | 2022-07-14 | 2024-01-18 | Rise Research Institutes of Sweden AB | Dispositif de traitement de substance |
| WO2024012887A1 (fr) * | 2022-07-14 | 2024-01-18 | Rise Research Institutes of Sweden AB | Dispositif de traitement de substance |
| KR102623046B1 (ko) | 2023-04-05 | 2024-01-10 | 고등기술연구원연구조합 | 윅구조를 포함하는 직접 접촉식 스팀 제너레이터 |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1296367A (en) * | 1916-04-08 | 1919-03-04 | Thomas Cochran | Process and apparatus for cracking and distilling hydrocarbons. |
| FR638779A (fr) | 1927-11-17 | 1928-06-02 | Armstrong Siddeley Motors Ltd | Perfectionnements aux moteurs à combustion interne |
| GB328339A (en) | 1929-02-01 | 1930-05-01 | Nicolai Alexeevich Kalabin | A method of and apparatus for producing a steam and gas mixture of high pressure |
| US1898086A (en) * | 1930-06-12 | 1933-02-21 | Foster Wheeler Corp | Pulverizing apparatus |
| US2512259A (en) * | 1943-04-09 | 1950-06-20 | Robert D Pike | Furnace for the production of nitric oxide from air |
| US2916877A (en) | 1954-05-12 | 1959-12-15 | Worthington Corp | Pressure fluid generator |
| US3378244A (en) * | 1966-01-12 | 1968-04-16 | Dresser Ind | Pebble heat exchanger |
| DE1533861B1 (de) * | 1966-04-16 | 1972-03-09 | Nippon Kokan Kk | Cowper-Winderhitzer |
| US3493344A (en) * | 1966-12-21 | 1970-02-03 | John C St Clair | Revolving pebble bed heat exchanger |
| US4398604A (en) | 1981-04-13 | 1983-08-16 | Carmel Energy, Inc. | Method and apparatus for producing a high pressure thermal vapor stream |
| JPS58115357A (ja) | 1981-12-29 | 1983-07-09 | Yamatake Honeywell Co Ltd | ガス用カロリ−メ−タ |
| US4463803A (en) | 1982-02-17 | 1984-08-07 | Trans Texas Energy, Inc. | Downhole vapor generator and method of operation |
| RU2285199C2 (ru) | 2004-12-21 | 2006-10-10 | Олег Петрович Кряжевских | Паровой котел с вращающимся парогенератором |
-
2008
- 2008-02-26 US US12/037,703 patent/US7814867B2/en not_active Expired - Fee Related
-
2009
- 2009-02-26 CA CA2655353A patent/CA2655353C/fr active Active
-
2010
- 2010-02-26 CA CA2694847A patent/CA2694847C/fr active Active
Also Published As
| Publication number | Publication date |
|---|---|
| US20090211539A1 (en) | 2009-08-27 |
| CA2694847A1 (fr) | 2010-08-26 |
| CA2655353C (fr) | 2019-07-09 |
| CA2655353A1 (fr) | 2009-08-26 |
| US7814867B2 (en) | 2010-10-19 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request |
Effective date: 20150223 |